JP2003164737A - Washing method for separation membrane and washing apparatus adapted thereto - Google Patents

Washing method for separation membrane and washing apparatus adapted thereto

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Publication number
JP2003164737A
JP2003164737A JP2001365978A JP2001365978A JP2003164737A JP 2003164737 A JP2003164737 A JP 2003164737A JP 2001365978 A JP2001365978 A JP 2001365978A JP 2001365978 A JP2001365978 A JP 2001365978A JP 2003164737 A JP2003164737 A JP 2003164737A
Authority
JP
Japan
Prior art keywords
separation membrane
cleaning
membrane
vibration
washing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2001365978A
Other languages
Japanese (ja)
Inventor
Norihiro Yaide
乃大 矢出
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ebara Corp
Original Assignee
Ebara Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ebara Corp filed Critical Ebara Corp
Priority to JP2001365978A priority Critical patent/JP2003164737A/en
Publication of JP2003164737A publication Critical patent/JP2003164737A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a washing method capable of effectively washing a separation membrane contaminated with organic or inorganic matter in a short time, and a washing apparatus adapted thereto. <P>SOLUTION: In the washing method for the separation membrane contaminated with organic matter and/or inorganic matter, the separation membrane is treated in a washing liquid by an ultra-vibration method and a contaminant is peeled and removed from the surface of the separation membrane to restore the separation capacity of the separation membrane. The washing apparatus for the separation membrane is constituted of a washing tank housing the separation membrane, a device for injecting the washing liquid in the washing tank and an ultra-vibration device arranged to the washing tank. The ultra-vibration device can be constituted of a vibration motor capable of being controlled to a frequency of 20-50 Hz, a vibration plate for accelerating vibration and multistage vibration blades attached to the vibration plate. <P>COPYRIGHT: (C)2003,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、分離膜の洗浄に係
り、特に、下水、し尿、産業排水等の排水処理や浄水処
理において、有機物や無機物で膜汚染された分離膜を洗
浄する方法と装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a separation membrane cleaning method, and more particularly, to a method for cleaning a separation membrane contaminated with an organic substance or an inorganic substance in wastewater treatment such as sewage, night soil, industrial wastewater, etc. or water purification treatment. Regarding the device.

【0002】[0002]

【従来の技術】分離膜は、下水、し尿、産業排水等や、
下水、し尿、産業排水等の排水処理や、半導体産業や医
薬製造業の用水処理や、浄水処理に広く使用されてい
る。分離膜は、懸濁物質や汚泥や凝集物及びバクテリア
除去の固液分離用に、限外ろ過膜(以下、UF膜)や精
密ろ過膜(以下、MF膜〕が、CODやBODや栄養塩
などの汚濁物質を除去するために、逆浸透膜(以下、R
O膜)やナノろ過膜(以下、NF膜)が使用されてい
る。RO膜やNF膜は、その孔径が分画分子量で千以下
と小さいために、200〜1500kPaの加圧条件下
で膜透過水を得る方式である。分離膜のうちUF膜とM
F膜は、運転管理が容易で、清澄な処理水が得られるこ
とから、沈殿槽のような重力分離に代わる固液分離方法
として、浄水処理やし尿処理、民間の小型廃水処理に普
及している。UF膜は、その孔径が分画分子量で千から
数十万であるために、被処理物に100〜500kPa
の圧力をかけて膜に通して、ろ過する方式である。MF
膜は、水槽に浸漬して、減圧条件下で透過水を得る方式
である。
2. Description of the Related Art Separation membranes are used for sewage, night soil, industrial wastewater, etc.
It is widely used for wastewater treatment such as sewage, night soil, industrial wastewater, water treatment for semiconductor industry and pharmaceutical manufacturing industry, and water purification treatment. Separation membranes include ultrafiltration membranes (hereinafter referred to as UF membranes) and microfiltration membranes (hereinafter referred to as MF membranes), COD, BOD and nutrient salts for solid-liquid separation for removal of suspended solids, sludge, aggregates and bacteria. Reverse osmosis membrane (hereinafter R
O membranes) and nanofiltration membranes (hereinafter, NF membranes) are used. Since the RO membrane and the NF membrane have a pore size as small as 1,000 or less in terms of molecular weight cutoff, they are a method of obtaining membrane permeated water under a pressure condition of 200 to 1500 kPa. UF membrane and M among separation membranes
Since the F membrane is easy to operate and manage and clear treated water can be obtained, it has become popular as a solid-liquid separation method instead of gravity separation such as in a settling tank for water purification treatment, night urine treatment, and private small wastewater treatment. There is. Since the UF membrane has a pore size of 1,000 to several hundred thousand in terms of molecular weight cut-off, the UF membrane has 100 to 500 kPa on the object to be treated.
It is a method of applying pressure to pass through a membrane and filtering. MF
The membrane is a system in which it is immersed in a water tank to obtain permeated water under reduced pressure conditions.

【0003】しかしながら、いずれの分離膜も使用を継
続すると、膜表面に被処理水の汚濁物質などが付着し、
分離膜で分離される膜透過水量が低下することになる。
膜透過水量が低下すると、計画処理水量が処理できず、
排水処理が困難になる。このような場合には、分離膜表
面の付着物を除去するための洗浄を行い、膜透過水量の
回復を図る。近年、排水処理や浄水処理における固液分
離膜として、MF膜を水槽に浸漬して使用する浸漬型M
F膜が普及している。図4に、浸漬型MF膜の使用形態
の概略構成図を示す。生物処理水槽流入水は、生物処理
水槽で槽内の活性汚泥により、流入水中の有機物が分解
除去される。処理水は、生物処理水槽内のMF膜を経由
して、モーノポンプなどの吸引ポンプにより水槽より排
出される。
However, if any separation membrane is used continuously, contaminants such as polluted water in the treated water adhere to the membrane surface,
The amount of permeated water separated by the separation membrane will decrease.
If the amount of membrane permeate decreases, the planned amount of treated water cannot be treated,
Wastewater treatment becomes difficult. In such a case, cleaning is performed to remove the deposits on the surface of the separation membrane to recover the amount of water permeated through the membrane. In recent years, as a solid-liquid separation membrane in wastewater treatment or water purification treatment, an immersion type M that uses an MF membrane by immersing it in a water tank
F-membrane is widespread. FIG. 4 shows a schematic configuration diagram of a usage pattern of the immersion type MF film. In the biological treated water inflow water, the organic matter in the inflow water is decomposed and removed by the activated sludge in the biological treated water tank. The treated water is discharged from the water tank by a suction pump such as a MONO pump via the MF membrane in the biological treatment water tank.

【0004】実用的なMF膜は、その孔径が0.1〜
0.4μm、材質がポリエチレン製で、中でも中空糸膜
が広く使用されている。複数の中空糸膜の両端を固定し
たものを膜エレメントとし、更に複数の膜エレメントを
ユニット化したものを膜モジュールとし、その膜モジュ
ールが生物反応水槽の水中に、必要数量が設置される。
又は、このMF膜は、透過水を得るための動力費を低減
するために、加圧条件でなく、膜内部を真空ポンプやモ
ーノポンプなどで減圧にして、膜外部から内部へと透過
水が移動して、処理水が得られる方式が一般的である。
膜の目詰まり状況は、膜間の差圧をモニターすることに
より判断できる。差圧は、水槽温度や透過水量によって
異なるが、概ね、−1〜−100kPa(ゲージ圧)で
ある。
A practical MF membrane has a pore size of 0.1 to 0.1.
0.4 μm, made of polyethylene, and hollow fiber membranes are widely used. A membrane element is formed by fixing both ends of a plurality of hollow fiber membranes, and a membrane module is formed by further uniting the plurality of membrane elements, and the required number of the membrane modules is installed in the water of the biological reaction water tank.
Alternatively, in order to reduce the power cost for obtaining the permeated water, this MF membrane does not require pressurization conditions, but the inside of the membrane is depressurized by a vacuum pump or a mohno pump, and the permeated water moves from the outside to the inside The general method is to obtain treated water.
The clogging condition of the membrane can be judged by monitoring the pressure difference between the membranes. The differential pressure is generally -1 to -100 kPa (gauge pressure), although it varies depending on the temperature of the water tank and the amount of permeated water.

【0005】差圧の上昇は、膜表面に堆積した汚泥など
による膜間閉塞と、膜の細孔が閉塞した膜汚染による
が、前者は簡単な水洗や空気洗浄により解消できる。後
者については、以下のとおりである。 (1) 分離膜を水槽から取り出して高圧水により洗浄
する。ただし、膜の損傷の可能性が高く、細孔内部の汚
染が十分に除去できない。 (2) 水槽から取り出した分離膜を洗浄槽に入れて、
洗浄剤を添加して、その洗浄液をポンプ循環、又は空気
攪拌して、分離膜を洗浄する。現状では、確実なろ過圧
解消方法である。しかし、このような方法では、洗浄に
要する時間が長かったり、洗浄効果が低かったり、洗浄
剤が過剰に必要である等の問題があった。
The increase in the differential pressure is due to the intermembrane clogging due to sludge accumulated on the membrane surface and the membrane contamination with the pores of the membrane clogging, but the former can be eliminated by simple water washing or air washing. The latter is as follows. (1) The separation membrane is taken out of the water tank and washed with high pressure water. However, there is a high possibility that the membrane will be damaged, and the contamination inside the pores cannot be sufficiently removed. (2) Put the separation membrane taken out of the water tank into the washing tank,
A cleaning agent is added, and the cleaning solution is circulated by pump or agitated with air to clean the separation membrane. At present, it is a reliable method of eliminating filtration pressure. However, in such a method, there are problems that the cleaning time is long, the cleaning effect is low, and the cleaning agent is excessive.

【0006】[0006]

【発明が解決しようとする課題】本発明は、上記従来技
術の問題点を解消し、有機物や無機物で膜汚染された分
離膜を、短時間に効果的に洗浄することができる分離膜
の洗浄方法と装置を提供することを課題とする。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems of the prior art and is capable of effectively cleaning a separation membrane contaminated with an organic substance or an inorganic substance in a short time. It is an object to provide a method and a device.

【0007】[0007]

【課題を解決するための手段】上記課題を解決するため
に、本発明では、有機物及び/又は無機物で膜汚染され
た分離膜の洗浄方法において、該分離膜を洗浄液中で超
振動法により処理し、分離膜表面から汚染物を剥離除去
して、分離性能を回復することを特徴とする分離膜の洗
浄方法としたものである。前記洗浄方法において、洗浄
液は、アルカリ剤、界面活性剤、酸化剤又は酸の少なく
とも1つの薬剤を含むことができる。また、本発明で
は、有機物及び/又は無機物で膜汚染された分離膜の洗
浄装置において、該分離膜を収容する洗浄槽と、該洗浄
槽に洗浄液を注入する装置と、該洗浄槽に配備した超振
動装置とからなることを特徴とする分離膜の洗浄装置と
したものである。前記洗浄装置において、超振動装置
は、周波数20〜50Hzに制御できる振動モータと、
振動を促進する振動板と、該振動板に取り付けた多段式
振動羽根とから構成することができる。
In order to solve the above problems, in the present invention, in a method for cleaning a separation membrane contaminated with an organic substance and / or an inorganic substance, the separation membrane is treated by a super vibration method in a cleaning liquid. Then, the method for cleaning the separation membrane is characterized in that the contaminants are peeled off from the surface of the separation membrane to recover the separation performance. In the cleaning method, the cleaning liquid may include at least one agent selected from an alkaline agent, a surfactant, an oxidizing agent, and an acid. Further, in the present invention, in a cleaning device for a separation membrane that is membrane-contaminated with an organic substance and / or an inorganic substance, a cleaning tank for containing the separation membrane, a device for injecting a cleaning liquid into the cleaning tank, and a cleaning tank are provided. A cleaning device for a separation membrane, which is characterized by comprising a super vibration device. In the cleaning device, the super vibration device is a vibration motor capable of controlling a frequency of 20 to 50 Hz,
It can be composed of a diaphragm that promotes vibration and multi-stage vibrating blades attached to the diaphragm.

【0008】[0008]

【発明の実施の形態】以下に、本発明を詳細に説明す
る。本発明の分離膜とは、下水、し尿、産業排水等や、
下水、し尿、産業排水等の排水処理や、用水処理及び浄
水処理に使用され、懸濁物質や汚泥や凝集物及びバクテ
リア除去の固液分離や、CODやBODや栄養塩などの
汚濁物質除去のための膜で、RO膜、NF膜、UF膜、
MF膜である。本発明における膜付着物は、特に限定さ
れないが、水酸化金属、金属酸化物、金属炭酸塩、金属
重炭酸塩、金属硫化物などの金属化合物、有機物や微生
物の集合体であるスライムなどであるが、膜表面や膜の
細孔内部に存在して、膜分離性能を低下させる物質の総
称である。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention is described in detail below. With the separation membrane of the present invention, sewage, night soil, industrial wastewater, and the like,
It is used for wastewater treatment such as sewage, night soil, industrial wastewater, water treatment and water purification, and solid-liquid separation for removing suspended solids, sludge, aggregates and bacteria, and removal of pollutants such as COD, BOD and nutrient salts. RO membrane, NF membrane, UF membrane,
It is an MF film. The film deposit in the present invention is not particularly limited, but may be a metal compound such as a metal hydroxide, a metal oxide, a metal carbonate, a metal bicarbonate, or a metal sulfide, or slime, which is an aggregate of organic substances and microorganisms. Is a general term for substances that exist on the surface of the membrane or inside the pores of the membrane and reduce the membrane separation performance.

【0009】本発明は、有機物や無機物で膜汚染された
分離膜の性能回復をする方法において、超振動法により
分離膜表面から汚染物を剥離除去する洗浄方法である。
図5に超振動洗浄装置の概略構成図を示す。超振動洗浄
方法は、低周波により激しい流動を発生させて、洗浄液
を激しく攪拌することで、振動と流動が同時に生じ、激
しい3次元の乱流攪拌が起こり、振動モータの振動が液
中に入った軸に上下に振動を伝えて、多段式振動羽根に
伝達される。堅い振動板に柔かい振動羽根をつけて、扇
のようにフラッタを生じさせて、さらに強い流動を生じ
させて、分離膜表面から汚染物を剥離除去するものであ
る。洗浄効果は、振動だけでなく、流動を伴った攪拌を
起こすために、洗浄効果が高い。二つの物理的な力の相
乗効果により、被洗浄物の細部まで洗浄が可能となる。
The present invention is a method for recovering the performance of a separation membrane contaminated with an organic substance or an inorganic substance, which is a cleaning method for removing contaminants from the surface of the separation membrane by a super vibration method.
FIG. 5 shows a schematic configuration diagram of the super vibration cleaning device. In the super vibration cleaning method, a violent flow is generated at a low frequency to vigorously stir the cleaning liquid, so that vibration and flow simultaneously occur, violent three-dimensional turbulent agitation occurs, and vibration of the vibration motor enters the liquid. The vibration is transmitted vertically to the shaft and transmitted to the multi-stage vibrating blade. By attaching a soft vibrating blade to a stiff diaphragm to generate flutter like a fan, a stronger flow is generated to remove contaminants from the surface of the separation membrane. The cleaning effect is high because not only vibration but also stirring accompanied by flow occurs. Due to the synergistic effect of the two physical forces, it is possible to clean the details of the object to be cleaned.

【0010】洗浄液が浸透し難い微細な穴や、強固に付
着した汚染物、被洗浄物である分離膜同士が密着した状
態など、極めて洗浄が困難な場合でも、優れた洗浄効果
が発揮できる。除去された汚染物が、微細化され洗浄液
中に安定化され、被洗浄物に再付着しない。また、超振
動洗浄装置の構造が簡単で、省スペースであり、大型や
小型などの分離膜の形状に適用可能である。図1〜図3
に、本発明の洗浄装置の概略構成図を示す。分離膜は、
図1のように、分離膜が設置されている場所に超振動洗
浄装置を搬入して、その場所で分離膜を取り外さずに洗
浄する場合と、図2及び図3のように、取り外した分離
膜を超振動洗浄装置が設置された洗浄水槽に入れて、洗
浄する方法があるが、いずれでも本発明が使用できる。
分離膜とフレームと配管などが組まれたモジュール毎、
あるいは分離膜そのものを、超振動洗浄装置で洗浄する
ことができる。
An excellent cleaning effect can be exhibited even in the case where cleaning is extremely difficult, such as in the case of minute holes in which the cleaning liquid does not easily penetrate, contaminants that are strongly adhered, and separation membranes that are the objects to be cleaned are in close contact with each other. The removed contaminants are made into fine particles, stabilized in the cleaning liquid, and do not reattach to the object to be cleaned. Further, the structure of the super-vibration cleaning device is simple and space-saving, and it can be applied to the shape of the separation membrane such as large and small. 1 to 3
FIG. 1 shows a schematic configuration diagram of the cleaning apparatus of the present invention. The separation membrane is
As shown in FIG. 1, the case where the super-vibration cleaning device is carried in to the place where the separation membrane is installed and the cleaning is performed at that place without removing the separation membrane, and the case where the separation membrane is removed as shown in FIGS. 2 and 3 There is a method of cleaning the membrane by putting it in a cleaning water tank equipped with a super-vibration cleaning device, and the present invention can be used in any case.
For each module that includes a separation membrane, frame, and piping,
Alternatively, the separation membrane itself can be washed with a super vibration washing device.

【0011】分離膜を浸漬させる液は、純水や工業用水
や容易に入手できる各種処理水が使用できる。また、分
離膜が設置された状態で洗浄する場合には、設置場所の
液、例えば活性汚泥や曝気槽混合液などが洗浄液に該当
する。また、本発明で用いる洗浄液は、アルカリ剤や界
面活性剤、酸化剤、酸の少なくとも1つの薬剤を含む洗
浄液を併用することができる。超振動洗浄方法と、アル
カリ剤や界面活性剤、酸化剤、酸の少なくとも1つの薬
剤を含む洗浄液を組み合わせて、より効果的に分離膜表
面から汚染物を剥離除去する。洗浄剤を併用することこ
とにより、微細な穴や強固に付着した汚染物にまで洗浄
剤が供給でき、洗浄効果を高めることができる。アルカ
リ剤は、苛性ソーダ、酸化剤は、次亜塩素酸ソーダなど
の塩素系酸化剤、過酸化水素、酸は、リン酸、シュウ
酸、クエン酸などの有機酸、界面活性剤は、ラウリル硫
酸ソーダなどの工業用洗剤や家庭用洗剤などである。
As a liquid for immersing the separation membrane, pure water, industrial water, or various kinds of easily available treated water can be used. When cleaning is performed with the separation membrane installed, the liquid at the installation location, such as activated sludge or aeration tank mixed liquid, corresponds to the cleaning liquid. Further, the cleaning liquid used in the present invention may be a cleaning liquid containing at least one chemical agent selected from an alkaline agent, a surfactant, an oxidizing agent and an acid. By combining the super-vibration cleaning method and a cleaning liquid containing at least one agent selected from an alkaline agent, a surfactant, an oxidizing agent and an acid, the contaminants can be more effectively peeled off from the surface of the separation membrane. By using the cleaning agent in combination, the cleaning agent can be supplied even to minute holes and firmly attached contaminants, and the cleaning effect can be enhanced. Alkali agents are caustic soda, oxidizing agents are chlorine-based oxidizing agents such as sodium hypochlorite, hydrogen peroxide, acids are organic acids such as phosphoric acid, oxalic acid and citric acid, and surfactants are sodium lauryl sulfate. Such as industrial detergents and household detergents.

【0012】一般的に、汚染物が、無機物なら酸が、有
機物なら酸化剤単独やアルカリ剤単独や界面活性剤単独
や、それらを混合した薬剤が使用される。また、アルカ
リ剤や界面活性剤で洗浄後、酸で洗浄する場合や、その
逆の場合もある。汚染物により任意に選択できる。分離
膜を変形しない範囲で、洗浄温度が高いと洗浄効果が高
いのは当然である。洗浄温度は20〜40℃が望まし
い。本発明は、洗浄液注入装置と超振動装置を配備した
洗浄槽からなる分離膜の洗浄装置である。洗浄液注入装
置は、洗浄剤貯槽と洗浄液注入ポンプから構成される。
超振動装置は、洗浄槽、振動モータ、振動を促進する振
動板、多段式振動羽根などから構成される。インバータ
を通して振動モータの周波数を20〜50Hzに制御す
ることにより、最適な洗浄強度が得られる。
In general, if the contaminant is an inorganic substance, an acid is used. If the contaminant is an organic substance, an oxidizing agent alone, an alkaline agent alone, a surfactant alone, or a mixture thereof is used. Further, after washing with an alkali agent or a surfactant, washing with an acid may be performed, and vice versa. It can be arbitrarily selected depending on the contaminant. It goes without saying that the washing effect is high if the washing temperature is high as long as the separation membrane is not deformed. The washing temperature is preferably 20 to 40 ° C. The present invention is a cleaning device for a separation membrane, which comprises a cleaning tank equipped with a cleaning liquid injection device and a super vibration device. The cleaning liquid injection device includes a cleaning agent storage tank and a cleaning liquid injection pump.
The super vibration device is composed of a cleaning tank, a vibration motor, a vibration plate that promotes vibration, a multi-stage vibration blade, and the like. Optimal cleaning strength can be obtained by controlling the frequency of the vibration motor to 20 to 50 Hz through the inverter.

【0013】[0013]

【実施例】以下に、本発明を実施例により具体的に説明
する。 実施例1 図4に示すような、計画水量が40m3/日の給食セン
ターの膜分離活性汚泥処理設備を用いて水処理をした。
該設備は、BOD負荷0.2kg/kg日、MLSS1
0g/l、原水BOD200mg/l、膜透過流束が
0.2m3/m2/日、MF膜(孔径0.1μm、ポリエ
チレン製)、膜面積が200m2である。1モジュール
が10m2で、20モジュールが膜分離活性汚泥処理水
槽に設置されている。この設備のMF膜を5%苛性ソー
ダと5%次亜塩素酸ソーダの洗浄液で洗浄後、約5ヶ月
が経過して、膜間の差圧が60kPaになり、透過水量
が低下した。MF膜が組み込まれた膜モジュール(1モ
ジュールが縦1m、横70cm)を取り外して、図2及
び図3の装置で洗浄試験を行った。
EXAMPLES The present invention will be specifically described below with reference to examples. Example 1 Water treatment was carried out using a membrane separation activated sludge treatment facility at a food service center having a planned water amount of 40 m 3 / day as shown in FIG.
The equipment has a BOD load of 0.2 kg / kg day and MLSS1.
0 g / l, raw water BOD 200 mg / l, membrane permeation flux 0.2 m 3 / m 2 / day, MF membrane (pore size 0.1 μm, made of polyethylene), membrane area 200 m 2 . One module is 10 m 2 and 20 modules are installed in the membrane separation activated sludge treatment water tank. Approximately 5 months after washing the MF membrane of this equipment with a washing solution of 5% sodium hydroxide and 5% sodium hypochlorite, the pressure difference between the membranes became 60 kPa and the amount of permeated water decreased. The membrane module (1 module was 1 m in length and 70 cm in width) in which the MF membrane was incorporated was removed, and a cleaning test was performed using the apparatus shown in FIGS. 2 and 3.

【0014】超振動装置は、1kwの振動モータで、幅
が20cmで全長が60cmの振動羽根が10cm間隔
に10枚取り付けられた、1本の振動板を振動させた。
超振動装置は、設置された洗浄水槽に水温25℃の水道
水1m3を入れ、この中に1モジュールあたりの膜面積
が10m2のモジュール1本を浸漬して10〜60分間
洗浄した。また、5%苛性ソーダと5%次亜塩素酸ソー
ダの洗浄液を用いて、洗浄液の滞留時間が10分間程度
で、洗浄液をポンプ循環して洗浄した。洗浄後のモジュ
ールを膜分離活性汚泥処理設備に取り付けて、分離膜の
性能を調査した。表1に、実施例1の試験結果を示す。
超振動単独でも、高い洗浄効果が認められた。さらに、
洗浄剤の添加によりMF膜の差圧の上昇を抑えることが
できた。
The super-vibration device was a vibration motor of 1 kW, and vibrated a single vibration plate having 10 vibration blades having a width of 20 cm and a total length of 60 cm, which were attached at intervals of 10 cm.
In the super vibration device, 1 m 3 of tap water having a water temperature of 25 ° C. was placed in the installed washing water tank, and one module having a membrane area of 10 m 2 per module was immersed in this for 10 to 60 minutes for washing. Further, using a cleaning solution of 5% caustic soda and 5% sodium hypochlorite, the cleaning solution was pumped and circulated for about 10 minutes for cleaning. The module after washing was attached to a membrane separation activated sludge treatment facility to investigate the performance of the separation membrane. Table 1 shows the test results of Example 1.
A high cleaning effect was observed even with super vibration alone. further,
By adding the cleaning agent, it was possible to suppress an increase in the differential pressure of the MF membrane.

【0015】[0015]

【表1】 [Table 1]

【0016】実施例2 実施例1の膜分離活性汚泥処理設備に組み込まれたモジ
ュールの1つを、塩ビ樹脂製の板で囲い、その中に実施
例1の超振動装置を設置し、図1の装置で洗浄試験を行
った。表2に、実施例2の試験結果を示す。生物処理水
槽の膜モジュールを取り外すことなく、その揚で洗浄が
でき、その効果は高い。膜分離活性汚泥処理水槽内で超
振動装置を使用して洗浄しても、その後の膜分離活性汚
泥処理に障害が生じなかった。
Example 2 One of the modules incorporated in the membrane-separated activated sludge treatment facility of Example 1 was surrounded by a vinyl chloride resin plate, and the super-vibration device of Example 1 was installed in the module. The cleaning test was conducted with the above apparatus. Table 2 shows the test results of Example 2. Without removing the membrane module of the biological treatment tank, it can be washed by lifting it, and its effect is high. Even when the membrane separation activated sludge treatment water tank was washed using an ultra-vibration device, no trouble occurred in the subsequent membrane separation activated sludge treatment.

【0017】[0017]

【表2】 [Table 2]

【0018】[0018]

【発明の効果】本発明の効果は以下の通りである。 (1) 少ない洗浄剤量又は短期間で高い洗浄効果が得
られる。 (2) 分離膜の細部まで洗浄ができて、長期間膜分離
性能が維持できる。 (3) 汚染物が再付着せず、膜の再汚染がない。 (4) 膜を取り外すことなく、その場所で膜の洗浄が
可能である。
The effects of the present invention are as follows. (1) A high cleaning effect can be obtained with a small amount of cleaning agent or in a short period of time. (2) The details of the separation membrane can be washed, and the membrane separation performance can be maintained for a long time. (3) Contaminants do not redeposit and there is no recontamination of the membrane. (4) The membrane can be cleaned at that location without removing it.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の洗浄装置の一例を示す概略構成図。FIG. 1 is a schematic configuration diagram showing an example of a cleaning apparatus of the present invention.

【図2】本発明の洗浄装置の他の例を示す概略構成図。FIG. 2 is a schematic configuration diagram showing another example of the cleaning apparatus of the present invention.

【図3】本発明の洗浄装置の他の例を示す概略構成図。FIG. 3 is a schematic configuration diagram showing another example of the cleaning apparatus of the present invention.

【図4】浸漬型MF膜を使用する生物処理水槽の概略構
成図。
FIG. 4 is a schematic configuration diagram of a biological treatment water tank using an immersion type MF membrane.

【図5】超振動洗浄装置の概略構成図。FIG. 5 is a schematic configuration diagram of a super vibration cleaning device.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 有機物及び/又は無機物で膜汚染された
分離膜の洗浄方法において、該分離膜を洗浄液中で超振
動法により処理し、分離膜表面から汚染物を剥離除去し
て、分離性能を回復することを特徴とする分離膜の洗浄
方法。
1. A method for cleaning a separation membrane contaminated with an organic substance and / or an inorganic substance, wherein the separation membrane is treated by a super vibration method in a cleaning liquid to remove contaminants from the surface of the separation membrane to separate the membrane. A method for cleaning a separation membrane, which comprises recovering
【請求項2】 前記洗浄液は、アルカリ剤、界面活性
剤、酸化剤又は酸の少なくとも1つの薬剤を含むことを
特徴とする請求項1記載の分離膜の洗浄方法。
2. The method for cleaning a separation membrane according to claim 1, wherein the cleaning liquid contains at least one agent selected from an alkaline agent, a surfactant, an oxidizing agent, and an acid.
【請求項3】 有機物及び/又は無機物で膜汚染された
分離膜の洗浄装置において、該分離膜を収容する洗浄槽
と、該洗浄槽に洗浄液を注入する装置と、該洗浄槽に配
備した超振動装置とからなることを特徴とする分離膜の
洗浄装置。
3. A cleaning device for a separation membrane, which is contaminated with an organic substance and / or an inorganic substance, in a cleaning tank for accommodating the separation membrane, a device for injecting a cleaning liquid into the cleaning tank, and a super tank provided in the cleaning tank. A cleaning device for a separation membrane, which comprises a vibrating device.
【請求項4】 前記超振動装置は、周波数20〜50H
zに制御できる振動モータと、振動を促進する振動板
と、該振動板に取り付けた多段式振動羽根とから構成さ
れることを特徴とする請求項3記載の分離膜の洗浄装
置。
4. The super vibration device has a frequency of 20 to 50H.
4. The separation membrane cleaning apparatus according to claim 3, comprising a vibration motor that can be controlled to z, a vibration plate that promotes vibration, and a multistage vibration blade that is attached to the vibration plate.
JP2001365978A 2001-11-30 2001-11-30 Washing method for separation membrane and washing apparatus adapted thereto Pending JP2003164737A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001365978A JP2003164737A (en) 2001-11-30 2001-11-30 Washing method for separation membrane and washing apparatus adapted thereto

Publications (1)

Publication Number Publication Date
JP2003164737A true JP2003164737A (en) 2003-06-10

Family

ID=19175943

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2003164737A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006043558A (en) * 2004-08-03 2006-02-16 Nihon Choriki Method of using water resource for school lunch, and system therefor
KR101495601B1 (en) * 2013-04-24 2015-02-26 위덕대학교 산학협력단 Membrane regenerating apparatus
JP2015097991A (en) * 2013-11-19 2015-05-28 栗田工業株式会社 Cleaning agent and cleaning method of permeable membrane
CN107617341A (en) * 2017-10-16 2018-01-23 陈永石 The membrane module cleaning device that processing is spent can be improved

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006043558A (en) * 2004-08-03 2006-02-16 Nihon Choriki Method of using water resource for school lunch, and system therefor
KR101495601B1 (en) * 2013-04-24 2015-02-26 위덕대학교 산학협력단 Membrane regenerating apparatus
JP2015097991A (en) * 2013-11-19 2015-05-28 栗田工業株式会社 Cleaning agent and cleaning method of permeable membrane
CN107617341A (en) * 2017-10-16 2018-01-23 陈永石 The membrane module cleaning device that processing is spent can be improved

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